JP2977595B2 - Syndiotactic polypropylene molded article and method for producing the same - Google Patents
Syndiotactic polypropylene molded article and method for producing the sameInfo
- Publication number
- JP2977595B2 JP2977595B2 JP2269383A JP26938390A JP2977595B2 JP 2977595 B2 JP2977595 B2 JP 2977595B2 JP 2269383 A JP2269383 A JP 2269383A JP 26938390 A JP26938390 A JP 26938390A JP 2977595 B2 JP2977595 B2 JP 2977595B2
- Authority
- JP
- Japan
- Prior art keywords
- syndiotactic
- small amount
- molded article
- polypropylene
- melting point
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C67/00—Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00
- B29C67/24—Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00 characterised by the choice of material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/10—Polymers of propylene
- B29K2023/12—PP, i.e. polypropylene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
- B29K2995/0018—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds having particular optical properties, e.g. fluorescent or phosphorescent
- B29K2995/0026—Transparent
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/04—Monomers containing three or four carbon atoms
- C08F110/06—Propene
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/26—Web or sheet containing structurally defined element or component, the element or component having a specified physical dimension
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Polymers & Plastics (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Treatments Of Macromolecular Shaped Articles (AREA)
- Heating, Cooling, Or Curing Plastics Or The Like In General (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明はシンジオタクチックポリプロピレン成形体お
よびその製造方法に関する。詳しくは、タクティシティ
ーの高いシンジオタクチックポリプロピレンあるいは共
重合体あるいは共重合体とアイソタクチックポリプロピ
レンとの混合物を成形して得た透明性に優れ、しかも剛
性と耐衝撃性のバランスに優れた成形体およびその成形
方法に関する。The present invention relates to a syndiotactic polypropylene molded article and a method for producing the same. For more information, molding with high tacticity syndiotactic polypropylene or a copolymer or a mixture of copolymer and isotactic polypropylene with excellent transparency and excellent balance between rigidity and impact resistance And a method of molding the same.
シンジオタクチックポリプロピレンについては古くよ
りその存在は知られていたが、従来のバナジウム化合物
とエーテルおよび有機アルミニウムからなる触媒で低温
重合させる方法はシンジオタクティシティーが悪く、エ
ラストマー的な特性を有すると言われているものの、そ
れが本来的にシンジオタクチックなポリプロピレンの特
徴を表しているとは言い難かった。これに対して、J.A.
EWENらにより非対称な配位子を有する遷移金属化合物と
アルミノキサンからなる触媒によってシンジオタクチッ
クペンタッド分率が0.7を越えるようなタクティシティ
ーの良好なポリプロピレンが得られることが初めて発見
された(J.Am.Chem.Soc.,1988,110,6255−6256)。Syndiotactic polypropylene has been known for a long time, but the conventional method of polymerizing at low temperature with a catalyst comprising a vanadium compound, ether and organoaluminum is said to have poor syndiotacticity and elastomeric properties. However, it was hard to say that it inherently characterizes syndiotactic polypropylene. In contrast, JA
EWEN et al. Discovered for the first time that a catalyst comprising a transition metal compound having an asymmetric ligand and an aluminoxane could produce a polypropylene having good tacticity with a syndiotactic pentad fraction exceeding 0.7 (J. Am. Chem. Soc., 1988, 110, 6255-6256).
上記方法で得られたシンジオタクチックポリプロピレ
ンあるいは実質的にシンジオタクチック構造を有するプ
ロピレンと他のオレフィンとの共重合体を成形した物は
比較的透明性に優れているがその透明性はまだ充分とは
言えなかった。The molded product of the syndiotactic polypropylene obtained by the above method or a copolymer of propylene having substantially a syndiotactic structure and another olefin has relatively excellent transparency, but its transparency is still insufficient. I couldn't say.
本発明者らは上記問題を解決して透明性の良好なシン
ジオタクチックポリプロピレン成形体について鋭意探索
したところ、特定のものが極めて透明性に優れ、しかも
剛性と耐衝撃性のバランスに優れていることを見出し本
発明を完成した。The present inventors have solved the above-mentioned problems and have intensively searched for a syndiotactic polypropylene molded article having good transparency, and specific ones are extremely excellent in transparency, and also excellent in balance between rigidity and impact resistance. The inventors have found that the present invention has been completed.
即ち本発明は、実質的にシンジオタクチック構造であ
るプロピレンの単独重合体、あるいは少量の他のオレフ
ィンとの共重合体またはそれらと少量の実質的にアイソ
タクチック構造であるポリプロピレンとの混合物を加熱
溶融形成した後、急冷することによって、示差走査熱分
析法により10℃/minで昇温して測定したシンジオタクチ
ック構造のポリプロピレンに帰属される融点が実質的に
単一ピークであるような成形体、もしくはこの成形体を
ついで融点以下の温度に加熱処理して得た透明性の良好
なシンジオタクチックポリプロピレン成形体である。本
発明はまた上記成形体を製造する好適な方法であり、実
質的にシンジオタクチック構造であるプロピレンの単独
重合体、あるいは少量の他のオレフィンとの共重合体ま
たはそれらと少量のアイソタクチック構造であるポリプ
ロピレンとの混合物を加熱溶融成形した後100℃/min以
上で急冷するか、もしくは急冷につづいて融点以下の温
度に加熱処理することを特徴とする透明性の良好なシン
ジオタクチックポリプロピレン成形体の製造方法であ
る。That is, the present invention relates to a propylene homopolymer having a substantially syndiotactic structure, a copolymer with a small amount of another olefin, or a mixture thereof with a small amount of a polypropylene having a substantially isotactic structure. After being heated and melt-formed, by rapid cooling, the melting point attributed to the syndiotactic polypropylene measured at a temperature of 10 ° C./min by differential scanning calorimetry is substantially a single peak. This is a molded article or a syndiotactic polypropylene molded article having good transparency obtained by subsequently subjecting this molded article to a heat treatment at a temperature not higher than the melting point. The present invention is also a preferred method for producing the above-mentioned molded article, comprising a homopolymer of propylene having a substantially syndiotactic structure, a copolymer with a small amount of another olefin, or a small amount thereof with an isotactic. Syndiotactic polypropylene with good transparency, characterized in that a mixture with polypropylene having a structure is heated and melt-molded and then quenched at 100 ° C / min or higher, or heat-treated to a temperature below the melting point following quenching. This is a method for producing a molded article.
本発明において実質的にシンジオタクチック構造であ
るプロピレンの単独重合体とは、そのシンジオタクチッ
クペンタッド分率が0.5以上、好ましくは0.7以上である
ものをいゝ、また、少量の他のオレフィンとの共重合体
については、その13C−NMRスペクトルにおいて、20.2pp
mに観測されるピーク強度がプロピレン単位のメチル基
に帰属される全ピークの強度の分に対して0.3以上、好
ましくは0.5以上であるものをいう。尚、シンジオタク
チックペンタッド分率の算出方法はA.Zambelliら;Macro
molecules vol.8,687(1975)および同vol.6,925(197
3)に記載してあり、13C−NMRスペクトルはポリマーの
1,2,4−トリクロロベンゼン溶液についてテトラメチル
シランを基準として測定することによって得られる。In the present invention, a propylene homopolymer having a substantially syndiotactic structure means one having a syndiotactic pentad fraction of 0.5 or more, preferably 0.7 or more, and a small amount of another olefin. With respect to the copolymer with, in its 13 C-NMR spectrum, 20.2 pp
The peak intensity observed at m is 0.3 or more, preferably 0.5 or more, of the intensity of all peaks attributed to the methyl group of the propylene unit. The method for calculating the syndiotactic pentad fraction is described in A. Zambelli et al .; Macro
molecules vol.8,687 (1975) and vol.6,925 (197
3), the 13 C-NMR spectrum of the polymer
It is obtained by measuring a 1,2,4-trichlorobenzene solution based on tetramethylsilane.
本発明において実質的にシンジオタクチック構造であ
るプロピレンの単独重合体、あるいは少量の他のオレフ
ィンとの共重合体を製造するに用いる触媒としては、上
記文献に記載された化合物が例示できるが、例示とは異
なる構造の触媒であっても、プロピレンの単独重合を行
ったときシンジオタクチックペンタッド分率が0.7以上
のポリプロピレンを製造することができる触媒系であれ
ば利用できる。Examples of the catalyst used for producing a propylene homopolymer having a substantially syndiotactic structure or a copolymer with a small amount of another olefin in the present invention include the compounds described in the above-mentioned documents. Even if the catalyst has a structure different from that of the examples, any catalyst system that can produce a polypropylene having a syndiotactic pentad fraction of 0.7 or more when propylene is homopolymerized can be used.
非対称な配位子を有する遷移金属化合物としては上記
文献に記載されたイソプロピル(シクロペンタジエニル
−1−フルオレニル)ハフニウムジクロリド、あるいは
イソプロピル(シクロペンタジエニル−1−フルオレニ
ル)ジルコニウムジクロリドあるいはこれら遷移金属化
合物の塩素原子の少なくとも1つをアルキル基で置換し
たものなどが例示され、またアルミノキサントとして
は、 (式中Rは炭素数1〜3の炭化水素残基。)で表される
化合物が例示でき、特にRがメチル基であるメチルアミ
ノキサンでnが5以上、好ましくは10〜100のものが使
用される。上記遷移金属化合物に対するアルミノキサン
の使用割合としては10〜1000000モル倍、通常50〜5000
モル倍である。また重合条件については特に制限はなく
不活性媒体を用いる溶媒重合法、或いは実質的に不活性
媒体の存在しない塊上重合体、気相重合法が利用でき
る。重合温度としては−100〜200℃、重合圧力としては
常圧〜100kg/cm2−Gで行うのが一般的である。好まし
くは−100〜100℃、常圧〜50kg/cm2−Gである。Examples of the transition metal compound having an asymmetric ligand include isopropyl (cyclopentadienyl-1-fluorenyl) hafnium dichloride, isopropyl (cyclopentadienyl-1-fluorenyl) zirconium dichloride, and transition metals described in the above literature. Compounds in which at least one of the chlorine atoms of the compound is substituted with an alkyl group are exemplified. (Wherein R is a hydrocarbon residue having 1 to 3 carbon atoms). In particular, methylaminoxan wherein R is a methyl group and n is 5 or more, preferably 10 to 100 used. The use ratio of the aluminoxane to the transition metal compound is 10 to 100,000,000 mole times, usually 50 to 5000.
It is molar times. The polymerization conditions are not particularly limited, and a solvent polymerization method using an inert medium, a bulk polymer substantially free of an inert medium, and a gas phase polymerization method can be used. Generally, the polymerization is carried out at a temperature of -100 to 200 ° C. and at a pressure of normal pressure to 100 kg / cm 2 -G. Preferably, it is -100 to 100 ° C and normal pressure to 50 kg / cm 2 -G.
ここで共重合に用いる他のオレフィンとしてはエチレ
ンあるいは炭素数4〜20のα−オレフィンが例示でき具
体的にはブテン−1、ペンテン−1、ヘキセン−1、オ
クテン−1、4−メチルペンテン−1などが例示され
る。プロピレンに対する重合の割合としては通常20wt%
以下の他のオレフィンが共重合する条件で重合され、20
wt%を越えると、成形体の剛性が低下し好ましくない。
共重合を行なう際の条件としては特に制限はなく、通常
用いられている公知の条件をそのまゝ採用することがで
きる。また重合を実質的に一段重合で行うと、得られた
重合体は分子量分布が狭く135℃でゲルパーミエーショ
ンクロマトグラフィーで測定した重量平均分子量と数平
均分子量の比(以下、MW/MNと略記する)は通常1.5〜3.
5程度であるが、2種の遷移金属化合物(金属として例
えばジルコニウムとハフニウムなど2種類のものを用い
ると効果的である。)を用いたり、分子量の異なるもの
を2種以上混合するなどしてMW/MNが3.5以上であるよう
な広い分子量分布のものを製造することができ本発明に
利用することが好ましい。好ましい分子量としては、13
5℃テトラリン溶液で測定した極限粘度(以下、ηと略
記する。)として0.5〜5.0dl/g程度であるのが一般的で
ある。またシンジオタクチックポリプロピレンの一部、
例えば50wt%未満までをアイソタクチック構造のポリプ
ロピレンで代替することもでき、こうすることでより高
剛性の成形体を得ることも可能である。Examples of the other olefin used in the copolymerization include ethylene and α-olefins having 4 to 20 carbon atoms. Specific examples include butene-1, pentene-1, hexene-1, octene-1, and 4-methylpentene. 1 and the like. The ratio of polymerization to propylene is usually 20wt%
The following other olefins are polymerized under copolymerization conditions,
If the amount exceeds wt%, the rigidity of the molded body is undesirably reduced.
The conditions for performing the copolymerization are not particularly limited, and commonly used known conditions can be employed as they are. When the polymerization is carried out in substantially one-stage polymerization, the obtained polymer has a narrow molecular weight distribution and a ratio of the weight average molecular weight to the number average molecular weight measured by gel permeation chromatography at 135 ° C. (hereinafter abbreviated as MW / MN). Is usually 1.5-3.
It is about 5, but two kinds of transition metal compounds (for example, it is effective to use two kinds of metals such as zirconium and hafnium) or a mixture of two or more kinds having different molecular weights. It is possible to produce a product having a wide molecular weight distribution such that MW / MN is 3.5 or more, and it is preferable to use the present invention. Preferred molecular weight is 13
Generally, the intrinsic viscosity (hereinafter abbreviated as η) measured with a 5 ° C. tetralin solution is about 0.5 to 5.0 dl / g. Also part of syndiotactic polypropylene,
For example, up to less than 50% by weight can be replaced by polypropylene having an isotactic structure, whereby a molded article having higher rigidity can be obtained.
上記シンジオタクチックポリプロピレンあるいは混合
物は、ついで加熱溶融し特定の形状に成形される。成形
方法としては成形した後急冷することが可能である限り
制限は無く、押出成形法、射出成形法が採用できる。The above syndiotactic polypropylene or mixture is then heated and melted and formed into a specific shape. The molding method is not limited as long as it can be cooled rapidly after molding, and an extrusion molding method or an injection molding method can be adopted.
本発明において重要なのは成形体を溶融した状態から
100℃/min以上、好ましくは150〜1000℃/minの速度で急
冷することである。急冷する方法としては成形体に冷媒
を接触させるのが一般的であるが、比較的低温の雰囲気
中に溶融した樹脂を導入することでも行える。こうする
ことで急冷後の成形体を示差走査熱分析法によって10℃
/minで昇温して測定したシンジオタクチック構造のポリ
プロピレンに帰属される融点が実質的に単一ピークであ
るようにすることができる。成形体を溶融した状態から
100℃/min未満の速度で徐冷したものについて同じ昇温
速度で示差走査熱分析法によって測定すると、この融点
が単一ピークとしては現れず、第1図(c)にみられる
如く2本もしくはそれ以上のピークが観測される。ま
た、このように徐冷したものは、後記する比較例1ない
し5にみられるように透明性が十分でなく好ましくな
い。尚、急冷したものについて観測される実質的に単一
ピークである融点の位置は、通常の条件すなわち示差走
査熱分析法によって一度250℃で溶融したのち、10℃/mi
nで30℃まで降温し、再び10℃/minで昇温して測定した
時に現れる融点のピーク(2本〜3本観測される)のう
ち最高のピークの位置よりも低温側に観測されるのが通
常である。What is important in the present invention is from the molten state of the compact.
Rapid cooling at a rate of 100 ° C./min or more, preferably 150 to 1000 ° C./min. As a method of quenching, it is common to bring a coolant into contact with the molded body, but it can also be carried out by introducing a molten resin into a relatively low-temperature atmosphere. In this way, the compact after quenching can be cooled to 10 ° C by differential scanning calorimetry.
The melting point attributable to the polypropylene having the syndiotactic structure measured by raising the temperature at / min can be substantially a single peak. From the molten state of the compact
When measured by differential scanning calorimetry at the same heating rate for those cooled slowly at a rate of less than 100 ° C./min, this melting point does not appear as a single peak, but as two peaks as shown in FIG. 1 (c). Or more peaks are observed. Moreover, the one thus cooled slowly is not preferable because the transparency is not sufficient as shown in Comparative Examples 1 to 5 described later. Incidentally, the position of the melting point, which is substantially a single peak observed for the quenched product, is once melted at 250 ° C. by ordinary conditions, ie, differential scanning calorimetry, and then at 10 ° C./mi.
The temperature is lowered to 30 ° C with n, and the temperature is raised again at 10 ° C / min. The peak is observed at a lower temperature than the position of the highest peak among the peaks of melting point (2 to 3 observed). Is usually the case.
この溶融成形したのち急冷する際に結晶化核剤を利用
することも勿論可能である。It is of course possible to utilize a crystallization nucleating agent when quenching after the melt molding.
この急冷したままの成形体は透明性は極めて優れてい
るが、剛性が通常のものに比較して劣る。さらにこの成
形体を融点以下の温度に加熱することで透明性は殆ど損
なわずに剛性を大幅に向上させることが可能である。加
熱温度としては高い方が短時間ですむが通常50℃〜融点
程度の温度が一般的であり加熱時間としては数秒〜数時
間であり、比較的高温の方がより短い時間で効果的であ
る。通常100℃程度で〜数時間程度が目安である。Although the molded body in this quenched state has extremely excellent transparency, the rigidity is inferior to that of the usual one. Further, by heating the molded body to a temperature equal to or lower than the melting point, the rigidity can be greatly improved without substantially impairing the transparency. The higher the heating temperature, the shorter the time is required, but generally the temperature of about 50 ° C. to the melting point is generally used, and the heating time is several seconds to several hours, and the relatively high temperature is more effective in a shorter time. . The standard is about 100 ° C to several hours.
以下に実施例を示しさらに本発明を説明する。 Hereinafter, the present invention will be described with reference to Examples.
実施例1 常法にしたがって合成したイソプロピルシクロペンタ
ジエニル−1−フルオレンをリチウム化し、四塩化ジル
コニウムと反応させ再結晶することで得たイソプロピル
(シクロペンタジエニル−1−フルオレニル)ジルコニ
ウムジクロリド0.2gと東洋アクゾ(株)製メチルアルミ
ノキサン(重合度16.1)30gを内容積200のオートクレ
ーブ中のトルエン80に加え、プロピレンを重合圧力3k
g/cm2−G、20℃で2時間重合させてポリマーを得た。
ポリマーをメタノールとアセト酢酸メチルで脱灰処理し
塩酸水溶液で洗浄し、ついで濾過して5.6kgのシンズオ
タクチックポリプロピレンを得た。このポリプロピレン
は13C−NMRによればシンジオタクチックペンタッド分率
は0.935であり、135℃テトラリン溶液で測定したηは1.
45dl/g、1,2,4−トリクロロベンゼンで測定したMW/MNは
2.2であった。このポリプロピレンに公知の安定剤を加
え、押出機で造粒し、ついで200℃で溶融プレスして1mm
のシートにして0℃の水に投入して急冷した。尚この急
冷の際、シートの中心に挿入したセンサーにより降温速
度を測定したところ250℃/minであった。このシートに
ついて以下の物性を測定した。Example 1 0.2 g of isopropyl (cyclopentadienyl-1-fluorenyl) zirconium dichloride obtained by lithiation of isopropylcyclopentadienyl-1-fluorene synthesized according to a conventional method, reaction with zirconium tetrachloride and recrystallization. And 30 g of methylaluminoxane manufactured by Toyo Akzo Co., Ltd. (degree of polymerization 16.1) were added to toluene 80 in an autoclave having a volume of 200, and propylene was polymerized at a polymerization pressure of 3 k
Polymerization was performed at g / cm 2 -G at 20 ° C. for 2 hours to obtain a polymer.
The polymer was demineralized with methanol and methyl acetoacetate, washed with an aqueous hydrochloric acid solution, and then filtered to obtain 5.6 kg of Shinsotatactic polypropylene. According to 13 C-NMR, the polypropylene had a syndiotactic pentad fraction of 0.935, and η measured at 135 ° C. in a tetralin solution was 1.
MW / MN measured at 45 dl / g, 1,2,4-trichlorobenzene is
2.2. A known stabilizer was added to this polypropylene, granulated with an extruder, and then melt-pressed at 200 ° C. to obtain 1 mm
And quenched in water at 0 ° C. During this quenching, the temperature drop rate was measured by a sensor inserted at the center of the sheet and found to be 250 ° C./min. The following physical properties of this sheet were measured.
・曲げ剛性度 :kg/cm2 ASTM D−747(23℃) ・引張降伏強さ:kg/cm2 ASTM D−638(23℃) ・破断時伸び : % ASTM D−638(23℃) ・アイゾット(ノッチ付)衝撃強度:kg・cm/cm ASTM D−638(23℃、−10℃) ・ヘイズ : % ASTM D1003に準じた。・ Bending stiffness: kg / cm 2 ASTM D-747 (23 ° C) ・ Tensile yield strength: kg / cm 2 ASTM D-638 (23 ° C) ・ Elongation at break:% ASTM D-638 (23 ° C) Izod (with notch) impact strength: kg · cm / cm ASTM D-638 (23 ° C, -10 ° C) Haze:% According to ASTM D1003.
曲げ剛性度、引張降伏強さ、破断時伸び、アイゾット
衝撃強度(23℃、−10℃)はそれぞれ5800、240、507、
45、3.6であり、ヘイズは21であった。また、示差走査
熱量分析法で10℃/minで昇温して測定した溶融挙動を第
1図(a)に示すが、シンジオタクチック構造に帰属さ
れる融点は実質的に単一ピークとなっている。Flexural rigidity, tensile yield strength, elongation at break, Izod impact strength (23 ° C, -10 ° C) are 5800, 240, 507,
It was 45, 3.6 and the haze was 21. FIG. 1 (a) shows the melting behavior measured at 10 ° C./min by differential scanning calorimetry. The melting point attributed to the syndiotactic structure is substantially a single peak. ing.
このシートをさらに145℃に制御した電気炉に入れ30
分間加熱処理したところシートの物性は以下のようであ
り引張降伏強度、曲げ剛性度が向上している。曲げ剛性
度、引張降伏強さ、破断時伸び、アイゾット衝撃強度
(23℃、−10℃)はそれぞれ6800、280、43、45、3.4で
あり、ヘイズは24であった。また、示差走査熱分析法で
10℃/minで昇温して測定した溶融挙動を第1図(b)に
示す。This sheet is further placed in an electric furnace controlled at 145 ° C. for 30 minutes.
After heat treatment for minutes, the physical properties of the sheet are as follows, and the tensile yield strength and the bending rigidity are improved. The flexural rigidity, tensile yield strength, elongation at break, and Izod impact strength (23 ° C., −10 ° C.) were 6,800, 280, 43, 45, 3.4, respectively, and the haze was 24. In addition, differential scanning calorimetry
FIG. 1 (b) shows the melting behavior measured at a temperature rise of 10 ° C./min.
比較例1 実施例1において、プレスシートの冷却を通常の条
件、すなわちプレスシートを成形した状態で冷却するこ
とで80℃/minで冷却した他は同様に成形して物性を測定
したところ曲げ剛性度、引張降伏強さ、破断時伸び、ア
イゾット衝撃強度(23℃、−10℃)はそれぞれ6200、26
1、520、12.7、3.6であり、ヘイズは56であった。ま
た、実施例1と同様な条件で測定した示差走査熱量分析
法による溶融挙動を第1図(c)に示す。Comparative Example 1 In Example 1, except that the press sheet was cooled under a normal condition, that is, cooled at 80 ° C./min by cooling in a state where the press sheet was formed, the physical properties were measured in the same manner. Degree, tensile yield strength, elongation at break, Izod impact strength (23 ° C, -10 ° C) are 6200, 26
The haze was 56, 1,520, 12.7, 3.6. FIG. 1 (c) shows the melting behavior by the differential scanning calorimetry measured under the same conditions as in Example 1.
このシートを145℃で30分間加熱処理して物性を測定
したところ、曲げ剛性度は6400、引張降伏強さは265、
破断時伸び180、アイゾット衝撃強度(23℃、−10℃)
は12.7、3.4となり、物性は加熱処理により若干向上し
たが、ヘイズは61と不良のまゝであった。This sheet was subjected to a heat treatment at 145 ° C. for 30 minutes and its physical properties were measured. The flexural rigidity was 6400, the tensile yield strength was 265,
Elongation at break 180, Izod impact strength (23 ℃, -10 ℃)
Were 12.7 and 3.4, and the physical properties were slightly improved by the heat treatment, but the haze was 61, which was poor.
実施例2 重合の際にヘキセン−1を共存させた他は実施例1と
同様にしてヘキセン含量6wt%の共重合体を得た。この
共重合体は13C−NMRによれば20.2ppmに観測されるピー
ク強度がプロピレン単位のメチル基に帰属される全ピー
クの強度の和に対し0.75であり、したがって実質的にシ
ンジオタクチックな構造のものであった。実施例1と同
様にして共重合体を加熱溶融成形した後急冷することに
より得たシートについて物性を測定したところ曲げ剛性
度、引張降伏強さ、破断時伸び、アイゾット衝撃強度
(23℃、−10℃)はそれぞれ4800、200、633、45、3.8
であり、ヘイズは15であった。また、示差走査熱分析法
により10℃/minで昇温して測定したシンジオタクチック
構造のポリプロピレンに帰属される融点は実質的に単一
ピークとなっていた。更にこのシートを110℃で60分加
熱処理したところ曲げ剛性度、引張降伏強さ、破断時伸
び、アイゾット衝撃強度(23℃、−10℃)はそれぞれ51
00、230、520、45、3.2であり、ヘイズは18であった。Example 2 A copolymer having a hexene content of 6% by weight was obtained in the same manner as in Example 1 except that hexene-1 was used in the polymerization. This copolymer has a peak intensity observed at 20.2 ppm according to 13 C-NMR of 0.75 with respect to the sum of the intensities of all peaks attributed to the methyl group of the propylene unit, and is therefore substantially syndiotactic. It was of a structure. The physical properties of the sheet obtained by heating and melt-molding the copolymer in the same manner as in Example 1 and then quenching were measured, and the flexural rigidity, tensile yield strength, elongation at break, and Izod impact strength (23 ° C., − 10 ℃) is 4800, 200, 633, 45, 3.8 respectively
And the haze was 15. Further, the melting point attributed to the polypropylene having a syndiotactic structure, measured by differential scanning calorimetry at a temperature rise of 10 ° C./min, was substantially a single peak. When this sheet was heated at 110 ° C for 60 minutes, the flexural rigidity, tensile yield strength, elongation at break, and Izod impact strength (23 ° C, -10 ° C) were each 51.
00, 230, 520, 45, 3.2 and the haze was 18.
比較例2 実施例2において、プレスシートの冷却を通常の条
件、すなわちプレスシートを形成した状態で冷却するこ
とで85℃/minで冷却した他は同様に成形して物性を測定
したところ曲げ剛性度、引張降伏強さ、破断時伸び、ア
イゾット衝撃強度(23℃、−10℃)はそれぞれ5000、21
0、585、13.5、3.7であり、ヘイズは47であった。Comparative Example 2 In Example 2, the press sheet was cooled under normal conditions, that is, cooled at 85 ° C./min by cooling while forming the press sheet. Temperature, tensile yield strength, elongation at break, and Izod impact strength (23 ° C, -10 ° C) are 5000 and 21 respectively.
0, 585, 13.5, 3.7, and haze was 47.
実施例3 常法にしたがって合成したイソプロピルシクロペンタ
ジエニル−1−フルオレンをリチウム化し、四塩化ハフ
ニウム(ジルコニウムを5wt%含有する。)と反応させ
再結晶することで得たイソプロピル(シクロペンタジエ
ニル−1−フルオレニル)ハフニウムジクロリド0.1gと
実施例1で合成したイソプロピル(シクロペンタジエニ
ル−1−フルオレニル)ジルコニウムジクロリド0.1g、
東ソ−アクゾ(株)製メチルアルミノキサン(重合度1
6.1)30gを内容積200のオートクレーブ中のトルエン8
0に加え、プロピレンを重合圧力3kg/cm2−G、20℃で
2時間重合させてポリマーを得た。ポリマーをメタノー
ルとアセト酢酸メチルで脱灰処理し塩酸水溶液で洗浄
し、ついで濾過して4.6kgのシンジオタクシックポリプ
ロピレンを得た。このポリプロピレンのシンジオタクチ
ックペンタッド分率は0.904であり、ηは1.68dl/g、MW/
MNは5.2であった。このポリプロピレンを用い実施例1
と同様に、押出機で造粒し、200℃で溶融プレスして1mm
のシートにして0℃の水に投入して急冷した。尚この急
冷の際、シートの中心に挿入したセンサーにより高温速
度を測定したところ250℃/minであった。曲げ剛性度、
引張降伏強さ、破断時伸び、アイゾット衝撃強度(23
℃、−10℃)はそれぞれ5200、210、480、45、3.8であ
り、ヘイズは8.5であった。示差走査熱量分析法で10℃/
minで測定したシンジオタクチック構造のポリプロピレ
ンに帰属される融点は135.3℃の実質的に単一ピークで
あった。このシートをさらに130℃に制御した電気炉に
入れ30分間加熱処理したところシートの物性は以下のよ
うであり引張降伏強度、曲げ剛性度が向上している。曲
げ剛性度、引張降伏強さ、破断時伸び、アイゾット衝撃
強度(23℃、−10℃)はそれぞれ5800、245、43、45、
3.8であり、ヘイズは10.3であった。Example 3 Isopropylcyclopentadienyl-1-fluorene synthesized according to a conventional method was lithiated, reacted with hafnium tetrachloride (containing 5 wt% zirconium), and recrystallized to obtain isopropyl (cyclopentadienyl). 0.1 g of -1-fluorenyl) hafnium dichloride and 0.1 g of isopropyl (cyclopentadienyl-1-fluorenyl) zirconium dichloride synthesized in Example 1;
Methylaluminoxane manufactured by Toso-Akzo Co., Ltd.
6.1) 30 g of toluene 8 in an autoclave with an internal volume of 200
In addition to 0, propylene was polymerized at 20 ° C. for 2 hours at a polymerization pressure of 3 kg / cm 2 -G to obtain a polymer. The polymer was deashed with methanol and methyl acetoacetate, washed with an aqueous hydrochloric acid solution, and then filtered to obtain 4.6 kg of syndiotactic polypropylene. The syndiotactic pentad fraction of this polypropylene is 0.904, η is 1.68 dl / g, MW /
MN was 5.2. Example 1 using this polypropylene
Similarly, granulate with an extruder and melt-press at 200 ° C to 1mm
And quenched in water at 0 ° C. During this quenching, the high-temperature rate was measured by a sensor inserted at the center of the sheet and found to be 250 ° C./min. Bending stiffness,
Tensile yield strength, elongation at break, Izod impact strength (23
C, -10C) were 5200, 210, 480, 45, and 3.8, respectively, and the haze was 8.5. 10 ° C / differential scanning calorimetry
The melting point attributable to the syndiotactic polypropylene measured in min was a substantially single peak at 135.3 ° C. The sheet was further placed in an electric furnace controlled at 130 ° C. and heat-treated for 30 minutes. The properties of the sheet were as follows, and the tensile yield strength and the bending rigidity were improved. Flexural rigidity, tensile yield strength, elongation at break, Izod impact strength (23 ° C, -10 ° C) are 5800, 245, 43, 45, respectively.
3.8 and the haze was 10.3.
比較例3 実施例3において、プレスシートの冷却を通常の条
件、すなわちプレスシートを成形した状態で冷却するこ
とで80℃/minで冷却した他は同様に成形して物性を測定
したところ曲げ剛性度、引張降伏強さ、破断時伸び、ア
イゾット衝撃強度(23℃、−10℃)はそれぞれ5250、21
0、420、12.7、3.6であり、ヘイズは58であった。Comparative Example 3 In Example 3, the press sheet was cooled under normal conditions, that is, cooled at 80 ° C./min by cooling in a state where the press sheet was formed. Degree, tensile yield strength, elongation at break, Izod impact strength (23 ° C, -10 ° C) are 5250, 21
The values were 0, 420, 12.7, and 3.6, and the haze was 58.
実施例4 重合の際にヘキセン−1を共存させた他は実施例3と
同様にしてヘキセン含量6wt%の共重合体を得た。この
共重合体は13C−NMRによれば20.2ppmに観測されるピー
ク強度がプロピレン単位のメチル基に帰属される全ピー
クの強度の和に対し0.68であり、したがって実質的にシ
ンジオタクチックな構造のものであった。又、MW/MNは
4.5であった。実施例3と同様にして共重合体を加熱溶
融成形した後急冷することにより得たシートについて物
性を測定したとこを曲げ剛性度、引張降伏強さ、破断時
伸び、アイゾット衝撃強度(23℃、−10℃)はそれぞれ
4600、190、640、45、3.8であり、ヘイズは16であっ
た。また、示差走査熱分析法により10℃/minで昇温して
測定したシンジオタクチック構造のポリプロピレンに帰
属される融点は実質的に単一ピークであった。このシー
トをさらに110℃に制御した電気炉に入れ60分間加熱処
理したところ曲げ剛性度、引張降伏強さ、破断時伸び、
アイゾット衝撃強度(23℃、−10℃)はそれぞれ5100、
240、490、45、3.3であり、ヘイズは17であった。Example 4 A copolymer having a hexene content of 6% by weight was obtained in the same manner as in Example 3 except that hexene-1 was used in the polymerization. This copolymer has a peak intensity observed at 20.2 ppm according to 13 C-NMR of 0.68 with respect to the sum of the intensities of all peaks attributed to the methyl group of the propylene unit, and is therefore substantially syndiotactic. It was of a structure. Also, MW / MN
It was 4.5. The physical properties of the sheet obtained by heating and melt-molding the copolymer in the same manner as in Example 3 and then quenching were measured. The sheet was measured for flexural rigidity, tensile yield strength, elongation at break, Izod impact strength (23 ° C., -10 ℃)
They were 4600, 190, 640, 45 and 3.8, and the haze was 16. Further, the melting point attributed to the polypropylene having a syndiotactic structure, which was measured by raising the temperature at 10 ° C./min by differential scanning calorimetry, was substantially a single peak. This sheet was further placed in an electric furnace controlled at 110 ° C. and subjected to heat treatment for 60 minutes, whereupon the bending stiffness, tensile yield strength, elongation at break,
Izod impact strength (23 ℃, -10 ℃) is 5100,
240, 490, 45, 3.3 and the haze was 17.
比較例4 実施例4において、プレスシートの冷却を通常の条
件、すなわちプレスシートを成形した状態で冷却するこ
とで85℃/minで冷却した他は同様に成形して物性を測定
したところ曲げ剛性度、引張降伏強さ、破断時伸び、ア
イゾット衝撃強度(23℃、−10℃)はそれぞれ5100、22
0、460、18.5、3.7であり、ヘイズは44であった。Comparative Example 4 In Example 4, the press sheet was cooled under normal conditions, that is, cooled at 85 ° C./min by cooling in a state where the press sheet was formed. Degree, tensile yield strength, elongation at break, Izod impact strength (23 ° C, -10 ° C) are 5100, 22
They were 0, 460, 18.5, 3.7 and the haze was 44.
実施例5 実施例3で得たシンジオタクチックポリプロピレン90
重量部に対し市販のアイソタクチックポリプロピレン
(アイソタクチックペンタド分率0.962、ηは1.62dl/
g)10重量部を混合した。混合物のMW/MNは7.5であっ
た。この混合物について実施例1と同様に加熱溶融成形
した後急冷してシート状の成形体をつくった。このシー
トについて物性を測定したところ、曲げ剛性度、引張降
伏強さ、破断時伸び、アイゾット衝撃強度(23℃、−10
℃)はそれぞれ6800、260、150、14.5、3.0であり、ヘ
イズは24であった。示差走査熱量分析装置で実施例3と
同様に融点を測定したところシンジオタクチック構造の
ポリプロピレンに帰属される融点としては145.5℃の実
質的に単一のピークであり、アイソタクチック構造のポ
リプロピレンに帰属される融点として162.0℃であっ
た。このシートをさらに145℃に制御した電気炉に入れ3
0分間加熱処理したところシートの物性は以下のようで
あり、引張降伏強度、曲げ剛性度が向上している。曲げ
剛性度、引張降伏強さ、破断時伸び、アイゾット衝撃強
度(23℃、−10℃)はそれぞれ7900、295、45、15.4、
3.1であり、ヘイズは25であった。Example 5 Syndiotactic polypropylene 90 obtained in Example 3
To the parts by weight, a commercially available isotactic polypropylene (isotactic pentad fraction 0.962, η is 1.62 dl /
g) 10 parts by weight were mixed. The MW / MN of the mixture was 7.5. This mixture was heated and melt-molded in the same manner as in Example 1 and then rapidly cooled to form a sheet-like molded body. When physical properties of this sheet were measured, flexural rigidity, tensile yield strength, elongation at break, and Izod impact strength (23 ° C, -10
C) were 6,800, 260, 150, 14.5, and 3.0, respectively, and the haze was 24. The melting point was measured with a differential scanning calorimeter in the same manner as in Example 3. As a result, the melting point attributed to the syndiotactic polypropylene was a substantially single peak at 145.5 ° C. The assigned melting point was 162.0 ° C. This sheet is further placed in an electric furnace controlled at 145 ° C.
After heat treatment for 0 minutes, the physical properties of the sheet are as follows, and the tensile yield strength and the bending rigidity are improved. Flexural rigidity, tensile yield strength, elongation at break, Izod impact strength (23 ° C, -10 ° C) are 7900, 295, 45, 15.4,
3.1 and haze was 25.
比較例5 実施例5において、プレスシートの冷却を通常の条
件、すなわちプレスシートを成形した状態で冷却するこ
とで80℃/minで冷却した他は同様に成形して物性を測定
したところ曲げ剛性度、引張降伏強さ、破断時伸び、ア
イゾット衝撃強度(23℃、−10℃)はそれぞれ7300、26
8、64、13.3、2.8であり、ヘイズは75であった。Comparative Example 5 In Example 5, except that the press sheet was cooled under a normal condition, that is, cooled at 80 ° C./min by cooling in a state where the press sheet was formed, the physical properties were measured in the same manner. Degree, tensile yield strength, elongation at break, Izod impact strength (23 ° C, -10 ° C) are 7300 and 26, respectively.
8, 64, 13.3, 2.8 and the haze was 75.
本発明の成形体は極めて透明性が良好であり、しかも
物性バランスに優れているので工業的に特にフィルムや
シートとしての用途に極めて価値がある。The molded article of the present invention has extremely good transparency and excellent balance of physical properties, and therefore is extremely valuable industrially particularly for use as a film or sheet.
第1図は実施例1および比較例1の成形体を示差走査熱
量分析法で分析したポリマーの溶融挙動であり、(a)
は実施例1の加熱処理前、(b)は実施例1の加熱処理
後、(c)は比較例1に対応する。FIG. 1 shows the melting behavior of the polymer obtained by analyzing the molded products of Example 1 and Comparative Example 1 by differential scanning calorimetry, and FIG.
Corresponds to before the heat treatment of Example 1, (b) corresponds to after the heat treatment of Example 1, and (c) corresponds to Comparative Example 1.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C08L 23:10 (31)優先権主張番号 特願平2−11800 (32)優先日 平2(1990)1月23日 (33)優先権主張国 日本(JP) (58)調査した分野(Int.Cl.6,DB名) C08J 5/00 B29C 35/00 B29C 71/02 ──────────────────────────────────────────────────の Continuing on the front page (51) Int.Cl. 6 Identification code FI C08L 23:10 (31) Priority claim number Japanese Patent Application No. 2-11800 (32) Priority date Hei 2 (1990) January 23 ( 33) Priority country Japan (JP) (58) Fields studied (Int. Cl. 6 , DB name) C08J 5/00 B29C 35/00 B29C 71/02
Claims (8)
ロピレンの単独重合体、あるいは少量の他のオレフィン
との共重合体あるいはそれらと少量のアイソタクチック
構造であるポリプロピレンとの混合物を加熱溶融成形し
た後、急冷することによって、示差走査熱分析法により
10℃/minで昇温して測定したシンジオタクチック構造の
ポリプロピレンに帰属される融点が実質的に単一ピーク
である透明性の良好なシンジオタクチックポリプロピレ
ン成形体。1. Hot melt molding of a homopolymer of propylene having a substantially syndiotactic structure, a copolymer with a small amount of another olefin, or a mixture thereof with a small amount of polypropylene having an isotactic structure. And then quenched by differential scanning calorimetry.
A highly transparent syndiotactic polypropylene molded article having a substantially single peak melting point attributable to a syndiotactic polypropylene measured at a temperature rise of 10 ° C./min.
ロピレンの単独重合体、あるいは少量の他のオレフィン
との共重合体あるいはそれらと少量のアイソタクチック
構造であるポリプロピレンとの混合物を加熱溶融成形し
た後100℃/min以上で急冷することを特徴とする透明性
の良好なシンジオタクチックポリプロピレン成形体の製
造方法。2. Hot melt molding of a homopolymer of propylene having a substantially syndiotactic structure, a copolymer with a small amount of another olefin, or a mixture thereof with a small amount of a polypropylene having an isotactic structure. And then quenching at 100 ° C./min or more. A method for producing a syndiotactic polypropylene molded article having good transparency.
ロピレンの単独重合体、あるいは少量の他のオレフィン
との共重合体またはそれらと少量の実質的にアイソタク
チック構造であるポリプロピレンとの混合物を加熱溶融
成形した後、急冷することによって、示差走査熱分析法
により10℃/minで昇温して測定したシンジオタクチック
構造のポリプロピレンに帰属される融点が実質的に単一
ピークであるような成形体とし、ついで融点以下の温度
に加熱処理して得た透明性の良好なシンジオタクチック
ポリプロピレン成形体。3. A propylene homopolymer having a substantially syndiotactic structure, a copolymer with a small amount of another olefin, or a mixture thereof with a small amount of a polypropylene having a substantially isotactic structure. After heating and melt-molding, by quenching, the melting point attributed to polypropylene having a syndiotactic structure measured at a temperature of 10 ° C./min by differential scanning calorimetry is substantially a single peak. A syndiotactic polypropylene molded article having good transparency, which is formed into a molded article and then subjected to a heat treatment at a temperature not higher than the melting point.
ロピレンの単独重合体、あるいは少量の他のオレフィン
との共重合体またはそれらと少量の実質的にアイソタク
チック構造であるポリプロピレンとの混合物を加熱溶融
成形した後100℃/min以上で急冷し、ついで融点以下の
温度に加熱処理することを特徴とする透明性の良好なシ
ンジオタクチックポリプロピレン成形体の製造方法。4. A propylene homopolymer having a substantially syndiotactic structure, a copolymer with a small amount of another olefin or a mixture thereof with a small amount of a polypropylene having a substantially isotactic structure. A method for producing a syndiotactic polypropylene molded article having good transparency, characterized by quenching at 100 ° C./min or more after heat-melt molding, and then heat-treating to a temperature below the melting point.
ロピレンの単独重合体、あるいは少量の他のオレフィン
との共重合体であって、重量平均分子量と数平均分子量
の比が1.5〜3.5である重合体を加熱溶融成形した後、急
冷することによって、示差走査熱分析により10℃/minで
昇温して測定した融点が実質的に単一ピークである透明
性の良好なシンジオタクチックポリプロピレン成形体。5. A propylene homopolymer having a substantially syndiotactic structure or a copolymer with a small amount of another olefin, wherein the ratio of the weight average molecular weight to the number average molecular weight is 1.5 to 3.5. After heating and melt-molding the polymer, it is rapidly cooled, and the melting point measured at 10 ° C./min by differential scanning calorimetry is substantially a single peak. body.
ロピレンの単独重合体あるいは少量の他のオレフィンと
の共重合体であって、重量平均分子量と数平均分子量の
比が1.5〜3.5である重合体を加熱溶融成形した後100℃/
min以上で急冷することを特徴とする透明性の良好なシ
ンジオタクチックポリプロピレン成形体の製造方法。6. A homopolymer of propylene having a substantially syndiotactic structure or a copolymer with a small amount of another olefin, wherein the ratio of the weight average molecular weight to the number average molecular weight is 1.5 to 3.5. 100 ° C /
A method for producing a syndiotactic polypropylene molded article having good transparency, characterized by quenching at a rate of at least min.
ロピレンの単独重合体、あるいは少量の他のオレフィン
との共重合体であって、重量平均分子量と数平均分子量
の比が1.5〜3.5である重合体を加熱溶融成形した後、急
冷することによって、示差走査熱分析法により10℃/min
で昇温して測定した融点が実質的に単一ピークであるよ
うな成形体とし、ついで融点以下の温度に加熱処理して
得た透明性の良好なシンジオタクチックポリプロピレン
成形体。7. A homopolymer of propylene having a substantially syndiotactic structure or a copolymer with a small amount of another olefin, wherein the ratio of the weight average molecular weight to the number average molecular weight is 1.5 to 3.5. After heating and melt-molding the polymer, it is quenched to obtain a differential scanning calorimetry of 10 ° C / min.
A molded article having a melting point substantially equal to a single peak by raising the temperature, and then subjected to a heat treatment at a temperature not higher than the melting point to obtain a syndiotactic polypropylene molded article having good transparency.
ロピレンの単独重合体、あるいは少量の他のオレフィン
との共重合体であって、重量平均分子量と数平均分子量
の比が1.5〜3.5である重合体を加熱溶融成形した後100
℃/min以上で急冷し、ついで融点以下の温度に加熱処理
することを特徴とする透明性の良好なシンジオタクチッ
クポリプロピレン成形体の製造方法。8. A homopolymer of propylene having a substantially syndiotactic structure or a copolymer with a small amount of another olefin, wherein the ratio of the weight average molecular weight to the number average molecular weight is 1.5 to 3.5. 100 after heat melting and molding the polymer
A method for producing a syndiotactic polypropylene molded article having good transparency, characterized by quenching at a temperature of at least ℃ / min and then heat-treating to a temperature below the melting point.
Applications Claiming Priority (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29949889 | 1989-11-20 | ||
JP31514089 | 1989-12-06 | ||
JP2-11799 | 1990-01-23 | ||
JP1-315140 | 1990-01-23 | ||
JP2-11800 | 1990-01-23 | ||
JP1179990 | 1990-01-23 | ||
JP1180090 | 1990-01-23 | ||
JP1-299498 | 1990-01-23 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03250030A JPH03250030A (en) | 1991-11-07 |
JP2977595B2 true JP2977595B2 (en) | 1999-11-15 |
Family
ID=27455680
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2269383A Expired - Lifetime JP2977595B2 (en) | 1989-11-20 | 1990-10-09 | Syndiotactic polypropylene molded article and method for producing the same |
Country Status (7)
Country | Link |
---|---|
US (2) | US5591817A (en) |
EP (1) | EP0428972B1 (en) |
JP (1) | JP2977595B2 (en) |
KR (1) | KR940004817B1 (en) |
CA (1) | CA2030245C (en) |
DE (1) | DE69020865T2 (en) |
ES (1) | ES2075117T3 (en) |
Families Citing this family (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0466926B1 (en) * | 1989-04-11 | 1995-02-22 | MITSUI TOATSU CHEMICALS, Inc. | Syndiotactic polypropylene molding and method of producing the same |
US5260395A (en) * | 1990-04-09 | 1993-11-09 | Mitsui Toatsu Chemicals, Inc. | Method for molding syndiotactic polypropylene and molded article |
US5200131A (en) * | 1990-04-09 | 1993-04-06 | Mitsui Toatsu Chemicals, Inc. | Method for molding syndiotactic polypropylene |
CA2120315C (en) * | 1993-04-30 | 2001-05-15 | Joel L. Williams | Medical articles and process therefor |
US5340917A (en) * | 1993-05-07 | 1994-08-23 | Exxon Chemical Patents Inc. | Syndiotactic polypropylene, methods for producing amorphous syndiotactic polypropylene and applications thereof |
EP0650816A1 (en) * | 1993-10-28 | 1995-05-03 | Mitsui Toatsu Chemicals, Incorporated | Method for injection molding blends of syndiotactic polypropylene and isotactic polypropylene and molded products obtained thereby |
JPH07125064A (en) * | 1993-10-29 | 1995-05-16 | Mitsui Toatsu Chem Inc | Inflation molding of polypropylene |
US5510075A (en) * | 1993-11-04 | 1996-04-23 | Becton, Dickinson And Company | Mold process for syndiotactic polypropylene |
KR0159685B1 (en) * | 1995-01-19 | 1998-12-15 | 사토 아키오 | Multilayer molded article of polypropylene |
JP3274052B2 (en) * | 1995-08-02 | 2002-04-15 | ティコナ・ゲゼルシャフト・ミット・ベシュレンクテル・ハフツング | Heating roller fixing type electrostatic image developing toner |
US6531230B1 (en) * | 1998-01-13 | 2003-03-11 | 3M Innovative Properties Company | Color shifting film |
EP1026199A1 (en) * | 1999-02-03 | 2000-08-09 | Fina Research S.A. | Polyolefins and uses thereof |
US7998579B2 (en) * | 2002-08-12 | 2011-08-16 | Exxonmobil Chemical Patents Inc. | Polypropylene based fibers and nonwovens |
US7652092B2 (en) * | 2002-08-12 | 2010-01-26 | Exxonmobil Chemical Patents Inc. | Articles from plasticized thermoplastic polyolefin compositions |
US7622523B2 (en) * | 2002-08-12 | 2009-11-24 | Exxonmobil Chemical Patents Inc. | Plasticized polyolefin compositions |
US7652094B2 (en) | 2002-08-12 | 2010-01-26 | Exxonmobil Chemical Patents Inc. | Plasticized polyolefin compositions |
EP1530611B1 (en) * | 2002-08-12 | 2013-12-04 | ExxonMobil Chemical Patents Inc. | Plasticized polyolefin compositions |
US7531594B2 (en) * | 2002-08-12 | 2009-05-12 | Exxonmobil Chemical Patents Inc. | Articles from plasticized polyolefin compositions |
US8003725B2 (en) * | 2002-08-12 | 2011-08-23 | Exxonmobil Chemical Patents Inc. | Plasticized hetero-phase polyolefin blends |
US7271209B2 (en) * | 2002-08-12 | 2007-09-18 | Exxonmobil Chemical Patents Inc. | Fibers and nonwovens from plasticized polyolefin compositions |
US7700707B2 (en) | 2002-10-15 | 2010-04-20 | Exxonmobil Chemical Patents Inc. | Polyolefin adhesive compositions and articles made therefrom |
US7294681B2 (en) * | 2002-10-15 | 2007-11-13 | Exxonmobil Chemical Patents Inc. | Mutliple catalyst system for olefin polymerization and polymers produced therefrom |
US7541402B2 (en) * | 2002-10-15 | 2009-06-02 | Exxonmobil Chemical Patents Inc. | Blend functionalized polyolefin adhesive |
US8192813B2 (en) | 2003-08-12 | 2012-06-05 | Exxonmobil Chemical Patents, Inc. | Crosslinked polyethylene articles and processes to produce same |
US8389615B2 (en) * | 2004-12-17 | 2013-03-05 | Exxonmobil Chemical Patents Inc. | Elastomeric compositions comprising vinylaromatic block copolymer, polypropylene, plastomer, and low molecular weight polyolefin |
EP2275451B1 (en) * | 2005-05-18 | 2016-10-19 | Mitsui Chemicals, Inc. | Method for producing propylene-based copolymer |
WO2007011530A2 (en) | 2005-07-15 | 2007-01-25 | Exxonmobil Chemical Patents, Inc. | Elastomeric compositions |
JP6150578B2 (en) * | 2013-03-26 | 2017-06-21 | 日東電工株式会社 | Ventilation member |
KR102174575B1 (en) | 2016-07-21 | 2020-11-05 | 미쓰이 가가쿠 가부시키가이샤 | Polypropylene resin composition, and single and multilayer films |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE591537A (en) * | 1959-06-06 | |||
NL293193A (en) * | 1962-05-28 | 1900-01-01 | ||
JPS58142818A (en) * | 1982-02-19 | 1983-08-25 | Idemitsu Petrochem Co Ltd | Manufacture of polypropylene sheet |
EP0183103B1 (en) * | 1984-11-09 | 1988-08-03 | TERUMO KABUSHIKI KAISHA trading as TERUMO CORPORATION | Flat permeable membrane and method for manufacture thereof |
JPS61189920A (en) * | 1985-02-20 | 1986-08-23 | Idemitsu Petrochem Co Ltd | Thermoforming polypropylene sheet and its manufacture |
US4824629A (en) * | 1988-02-04 | 1989-04-25 | The Dow Chemical Company | Process for preparing an oriented crystalline syndiotactic vinylaromatic polymer |
US4892851A (en) * | 1988-07-15 | 1990-01-09 | Fina Technology, Inc. | Process and catalyst for producing syndiotactic polyolefins |
EP0419677B1 (en) * | 1989-04-18 | 1995-12-27 | MITSUI TOATSU CHEMICALS, Inc. | Syndiotactic polypropylene resin composition |
DE69023575T2 (en) * | 1989-08-24 | 1996-08-08 | Mitsui Toatsu Chemicals | New extruded films and foils made of polypropylene. |
US5200131A (en) * | 1990-04-09 | 1993-04-06 | Mitsui Toatsu Chemicals, Inc. | Method for molding syndiotactic polypropylene |
US5204037A (en) * | 1991-01-25 | 1993-04-20 | Idemitsu Petrochemical Co., Ltd. | Process for production of polypropylene sheets or films |
US5357014A (en) * | 1991-08-09 | 1994-10-18 | Idemitsu Kosan Co., Ltd. | Styrenic resin molding and process for producing same |
US5510075A (en) * | 1993-11-04 | 1996-04-23 | Becton, Dickinson And Company | Mold process for syndiotactic polypropylene |
-
1990
- 1990-10-09 JP JP2269383A patent/JP2977595B2/en not_active Expired - Lifetime
- 1990-11-07 KR KR1019900017983A patent/KR940004817B1/en not_active IP Right Cessation
- 1990-11-12 DE DE69020865T patent/DE69020865T2/en not_active Expired - Lifetime
- 1990-11-12 EP EP90121609A patent/EP0428972B1/en not_active Expired - Lifetime
- 1990-11-12 ES ES90121609T patent/ES2075117T3/en not_active Expired - Lifetime
- 1990-11-19 CA CA002030245A patent/CA2030245C/en not_active Expired - Fee Related
-
1994
- 1994-03-18 US US08/210,082 patent/US5591817A/en not_active Expired - Lifetime
-
1996
- 1996-09-25 US US08/719,514 patent/US5759469A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
EP0428972A3 (en) | 1992-03-11 |
KR940004817B1 (en) | 1994-06-01 |
US5591817A (en) | 1997-01-07 |
CA2030245C (en) | 1994-07-12 |
ES2075117T3 (en) | 1995-10-01 |
CA2030245A1 (en) | 1991-05-21 |
JPH03250030A (en) | 1991-11-07 |
EP0428972A2 (en) | 1991-05-29 |
US5759469A (en) | 1998-06-02 |
EP0428972B1 (en) | 1995-07-12 |
DE69020865D1 (en) | 1995-08-17 |
DE69020865T2 (en) | 1995-12-21 |
KR910009791A (en) | 1991-06-28 |
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